CN117488557A - Filter bag capable of inhibiting condensation and dust adhesion and processing technology thereof - Google Patents
Filter bag capable of inhibiting condensation and dust adhesion and processing technology thereof Download PDFInfo
- Publication number
- CN117488557A CN117488557A CN202410003748.0A CN202410003748A CN117488557A CN 117488557 A CN117488557 A CN 117488557A CN 202410003748 A CN202410003748 A CN 202410003748A CN 117488557 A CN117488557 A CN 117488557A
- Authority
- CN
- China
- Prior art keywords
- coating
- water
- agent
- repellent
- filter bag
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
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- 239000000428 dust Substances 0.000 title claims abstract description 97
- 238000009833 condensation Methods 0.000 title claims abstract description 72
- 230000005494 condensation Effects 0.000 title claims abstract description 72
- 230000002401 inhibitory effect Effects 0.000 title claims abstract description 71
- 238000005516 engineering process Methods 0.000 title claims abstract description 34
- 238000012545 processing Methods 0.000 title claims abstract description 34
- 239000005871 repellent Substances 0.000 claims abstract description 314
- 239000011248 coating agent Substances 0.000 claims abstract description 254
- 238000000576 coating method Methods 0.000 claims abstract description 254
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 220
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 154
- 239000010954 inorganic particle Substances 0.000 claims abstract description 153
- 239000002519 antifouling agent Substances 0.000 claims abstract description 98
- 238000003756 stirring Methods 0.000 claims abstract description 92
- 238000010438 heat treatment Methods 0.000 claims abstract description 54
- 238000005507 spraying Methods 0.000 claims abstract description 31
- 238000000034 method Methods 0.000 claims abstract description 22
- -1 polysiloxane Polymers 0.000 claims description 64
- 239000001913 cellulose Substances 0.000 claims description 39
- 235000010980 cellulose Nutrition 0.000 claims description 39
- 229920002678 cellulose Polymers 0.000 claims description 39
- 239000000839 emulsion Substances 0.000 claims description 39
- 229920001296 polysiloxane Polymers 0.000 claims description 38
- 238000006243 chemical reaction Methods 0.000 claims description 36
- 239000003349 gelling agent Substances 0.000 claims description 34
- 229920002554 vinyl polymer Polymers 0.000 claims description 32
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 30
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 claims description 30
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims description 26
- 229910052731 fluorine Inorganic materials 0.000 claims description 26
- 239000011737 fluorine Substances 0.000 claims description 26
- 239000008367 deionised water Substances 0.000 claims description 23
- 229910021641 deionized water Inorganic materials 0.000 claims description 23
- 229920000642 polymer Polymers 0.000 claims description 22
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 21
- 239000004205 dimethyl polysiloxane Substances 0.000 claims description 18
- 235000013870 dimethyl polysiloxane Nutrition 0.000 claims description 18
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 claims description 18
- 239000002159 nanocrystal Substances 0.000 claims description 15
- 230000008569 process Effects 0.000 claims description 14
- 239000000178 monomer Substances 0.000 claims description 13
- 238000004321 preservation Methods 0.000 claims description 13
- 239000005058 Isophorone diisocyanate Substances 0.000 claims description 12
- NIMLQBUJDJZYEJ-UHFFFAOYSA-N isophorone diisocyanate Chemical compound CC1(C)CC(N=C=O)CC(C)(CN=C=O)C1 NIMLQBUJDJZYEJ-UHFFFAOYSA-N 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 12
- 239000002202 Polyethylene glycol Substances 0.000 claims description 10
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 claims description 10
- UKLDJPRMSDWDSL-UHFFFAOYSA-L [dibutyl(dodecanoyloxy)stannyl] dodecanoate Chemical compound CCCCCCCCCCCC(=O)O[Sn](CCCC)(CCCC)OC(=O)CCCCCCCCCCC UKLDJPRMSDWDSL-UHFFFAOYSA-L 0.000 claims description 10
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 claims description 10
- 239000012975 dibutyltin dilaurate Substances 0.000 claims description 10
- 125000001301 ethoxy group Chemical group [H]C([H])([H])C([H])([H])O* 0.000 claims description 10
- STVZJERGLQHEKB-UHFFFAOYSA-N ethylene glycol dimethacrylate Chemical compound CC(=C)C(=O)OCCOC(=O)C(C)=C STVZJERGLQHEKB-UHFFFAOYSA-N 0.000 claims description 10
- 229920001223 polyethylene glycol Polymers 0.000 claims description 10
- RGPUVZXXZFNFBF-UHFFFAOYSA-K diphosphonooxyalumanyl dihydrogen phosphate Chemical compound [Al+3].OP(O)([O-])=O.OP(O)([O-])=O.OP(O)([O-])=O RGPUVZXXZFNFBF-UHFFFAOYSA-K 0.000 claims description 9
- HMMGMWAXVFQUOA-UHFFFAOYSA-N octamethylcyclotetrasiloxane Chemical compound C[Si]1(C)O[Si](C)(C)O[Si](C)(C)O[Si](C)(C)O1 HMMGMWAXVFQUOA-UHFFFAOYSA-N 0.000 claims description 9
- 229920002818 (Hydroxyethyl)methacrylate Polymers 0.000 claims description 8
- WOBHKFSMXKNTIM-UHFFFAOYSA-N Hydroxyethyl methacrylate Chemical compound CC(=C)C(=O)OCCO WOBHKFSMXKNTIM-UHFFFAOYSA-N 0.000 claims description 8
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 8
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 claims description 8
- DCUFMVPCXCSVNP-UHFFFAOYSA-N methacrylic anhydride Chemical compound CC(=C)C(=O)OC(=O)C(C)=C DCUFMVPCXCSVNP-UHFFFAOYSA-N 0.000 claims description 8
- 239000012299 nitrogen atmosphere Substances 0.000 claims description 8
- MSRJTTSHWYDFIU-UHFFFAOYSA-N octyltriethoxysilane Chemical compound CCCCCCCC[Si](OCC)(OCC)OCC MSRJTTSHWYDFIU-UHFFFAOYSA-N 0.000 claims description 8
- 229960003493 octyltriethoxysilane Drugs 0.000 claims description 8
- 238000002360 preparation method Methods 0.000 claims description 8
- SAMJGBVVQUEMGC-UHFFFAOYSA-N 1-ethenoxy-2-(2-ethenoxyethoxy)ethane Chemical compound C=COCCOCCOC=C SAMJGBVVQUEMGC-UHFFFAOYSA-N 0.000 claims description 7
- VMAWODUEPLAHOE-UHFFFAOYSA-N 2,4,6,8-tetrakis(ethenyl)-2,4,6,8-tetramethyl-1,3,5,7,2,4,6,8-tetraoxatetrasilocane Chemical compound C=C[Si]1(C)O[Si](C)(C=C)O[Si](C)(C=C)O[Si](C)(C=C)O1 VMAWODUEPLAHOE-UHFFFAOYSA-N 0.000 claims description 7
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 claims description 7
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 claims description 7
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 7
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 claims description 7
- GVGUFUZHNYFZLC-UHFFFAOYSA-N dodecyl benzenesulfonate;sodium Chemical compound [Na].CCCCCCCCCCCCOS(=O)(=O)C1=CC=CC=C1 GVGUFUZHNYFZLC-UHFFFAOYSA-N 0.000 claims description 7
- 238000004945 emulsification Methods 0.000 claims description 7
- 238000002390 rotary evaporation Methods 0.000 claims description 7
- 229940080264 sodium dodecylbenzenesulfonate Drugs 0.000 claims description 7
- 229940080352 sodium stearoyl lactylate Drugs 0.000 claims description 7
- ODFAPIRLUPAQCQ-UHFFFAOYSA-M sodium stearoyl lactylate Chemical compound [Na+].CCCCCCCCCCCCCCCCCC(=O)OC(C)C(=O)OC(C)C([O-])=O ODFAPIRLUPAQCQ-UHFFFAOYSA-M 0.000 claims description 7
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 6
- 239000003054 catalyst Substances 0.000 claims description 6
- DKPFZGUDAPQIHT-UHFFFAOYSA-N Butyl acetate Natural products CCCCOC(C)=O DKPFZGUDAPQIHT-UHFFFAOYSA-N 0.000 claims description 5
- 229910001870 ammonium persulfate Inorganic materials 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 5
- 238000004108 freeze drying Methods 0.000 claims description 5
- FUZZWVXGSFPDMH-UHFFFAOYSA-N hexanoic acid Chemical compound CCCCCC(O)=O FUZZWVXGSFPDMH-UHFFFAOYSA-N 0.000 claims description 5
- 230000003301 hydrolyzing effect Effects 0.000 claims description 5
- 238000009413 insulation Methods 0.000 claims description 5
- 230000007935 neutral effect Effects 0.000 claims description 5
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 claims description 5
- 238000010992 reflux Methods 0.000 claims description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 4
- 229920000168 Microcrystalline cellulose Polymers 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- 229940016286 microcrystalline cellulose Drugs 0.000 claims description 4
- 235000019813 microcrystalline cellulose Nutrition 0.000 claims description 4
- 239000008108 microcrystalline cellulose Substances 0.000 claims description 4
- 230000001105 regulatory effect Effects 0.000 claims description 4
- 239000005457 ice water Substances 0.000 claims description 3
- 239000004408 titanium dioxide Substances 0.000 claims description 3
- 238000005406 washing Methods 0.000 claims description 3
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 2
- 229920002313 fluoropolymer Polymers 0.000 claims description 2
- 239000004811 fluoropolymer Substances 0.000 claims description 2
- 239000004745 nonwoven fabric Substances 0.000 claims description 2
- 238000006068 polycondensation reaction Methods 0.000 claims description 2
- 239000000377 silicon dioxide Substances 0.000 claims description 2
- 235000012239 silicon dioxide Nutrition 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims 7
- 239000000126 substance Substances 0.000 description 26
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 24
- 239000003921 oil Substances 0.000 description 15
- 230000000052 comparative effect Effects 0.000 description 14
- 238000012360 testing method Methods 0.000 description 13
- 230000000694 effects Effects 0.000 description 8
- 239000004810 polytetrafluoroethylene Substances 0.000 description 8
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 8
- 230000002940 repellent Effects 0.000 description 8
- 239000000463 material Substances 0.000 description 7
- 238000007865 diluting Methods 0.000 description 6
- 230000002209 hydrophobic effect Effects 0.000 description 6
- 239000002245 particle Substances 0.000 description 5
- 230000003373 anti-fouling effect Effects 0.000 description 4
- 238000007598 dipping method Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- JJUBFBTUBACDHW-UHFFFAOYSA-N 3,3,4,4,5,5,6,6,7,7,8,8,9,9,10,10,10-heptadecafluoro-1-decanol Chemical compound OCCC(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F JJUBFBTUBACDHW-UHFFFAOYSA-N 0.000 description 3
- 238000010790 dilution Methods 0.000 description 3
- 239000012895 dilution Substances 0.000 description 3
- 230000001804 emulsifying effect Effects 0.000 description 3
- 238000011156 evaluation Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 238000006116 polymerization reaction Methods 0.000 description 3
- 150000003242 quaternary ammonium salts Chemical group 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 238000010025 steaming Methods 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000002035 prolonged effect Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 230000006641 stabilisation Effects 0.000 description 2
- 238000011105 stabilization Methods 0.000 description 2
- 230000002195 synergetic effect Effects 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000005903 acid hydrolysis reaction Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- FWDBOZPQNFPOLF-UHFFFAOYSA-N ethenyl(triethoxy)silane Chemical compound CCO[Si](OCC)(OCC)C=C FWDBOZPQNFPOLF-UHFFFAOYSA-N 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000007888 film coating Substances 0.000 description 1
- 238000009501 film coating Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000006459 hydrosilylation reaction Methods 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- IQPQWNKOIGAROB-UHFFFAOYSA-N isocyanate group Chemical group [N-]=C=O IQPQWNKOIGAROB-UHFFFAOYSA-N 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 239000002086 nanomaterial Substances 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 230000003746 surface roughness Effects 0.000 description 1
- RRHXZLALVWBDKH-UHFFFAOYSA-M trimethyl-[2-(2-methylprop-2-enoyloxy)ethyl]azanium;chloride Chemical compound [Cl-].CC(=C)C(=O)OCC[N+](C)(C)C RRHXZLALVWBDKH-UHFFFAOYSA-M 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0001—Making filtering elements
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B3/00—Preparation of cellulose esters of organic acids
- C08B3/08—Preparation of cellulose esters of organic acids of monobasic organic acids with three or more carbon atoms, e.g. propionate or butyrate
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F251/00—Macromolecular compounds obtained by polymerising monomers on to polysaccharides or derivatives thereof
- C08F251/02—Macromolecular compounds obtained by polymerising monomers on to polysaccharides or derivatives thereof on to cellulose or derivatives thereof
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F283/00—Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G
- C08F283/12—Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to polysiloxanes
- C08F283/124—Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to polysiloxanes on to polysiloxanes having carbon-to-carbon double bonds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/2805—Compounds having only one group containing active hydrogen
- C08G18/288—Compounds containing at least one heteroatom other than oxygen or nitrogen
- C08G18/2885—Compounds containing at least one heteroatom other than oxygen or nitrogen containing halogen atoms
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/67—Unsaturated compounds having active hydrogen
- C08G18/671—Unsaturated compounds having only one group containing active hydrogen
- C08G18/672—Esters of acrylic or alkyl acrylic acid having only one group containing active hydrogen
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
- C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
- C08G18/75—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic
- C08G18/751—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic containing only one cycloaliphatic ring
- C08G18/752—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic containing only one cycloaliphatic ring containing at least one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group
- C08G18/753—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic containing only one cycloaliphatic ring containing at least one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group containing one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group having a primary carbon atom next to the isocyanate or isothiocyanate group
- C08G18/755—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic containing only one cycloaliphatic ring containing at least one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group containing one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group having a primary carbon atom next to the isocyanate or isothiocyanate group and at least one isocyanate or isothiocyanate group linked to a secondary carbon atom of the cycloaliphatic ring, e.g. isophorone diisocyanate
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
- C08G77/42—Block-or graft-polymers containing polysiloxane sequences
- C08G77/46—Block-or graft-polymers containing polysiloxane sequences containing polyether sequences
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06N—WALL, FLOOR, OR LIKE COVERING MATERIALS, e.g. LINOLEUM, OILCLOTH, ARTIFICIAL LEATHER, ROOFING FELT, CONSISTING OF A FIBROUS WEB COATED WITH A LAYER OF MACROMOLECULAR MATERIAL; FLEXIBLE SHEET MATERIAL NOT OTHERWISE PROVIDED FOR
- D06N3/00—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof
- D06N3/0002—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof characterised by the substrate
- D06N3/0011—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof characterised by the substrate using non-woven fabrics
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06N—WALL, FLOOR, OR LIKE COVERING MATERIALS, e.g. LINOLEUM, OILCLOTH, ARTIFICIAL LEATHER, ROOFING FELT, CONSISTING OF A FIBROUS WEB COATED WITH A LAYER OF MACROMOLECULAR MATERIAL; FLEXIBLE SHEET MATERIAL NOT OTHERWISE PROVIDED FOR
- D06N3/00—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof
- D06N3/0056—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof characterised by the compounding ingredients of the macro-molecular coating
- D06N3/0059—Organic ingredients with special effects, e.g. oil- or water-repellent, antimicrobial, flame-resistant, magnetic, bactericidal, odour-influencing agents; perfumes
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06N—WALL, FLOOR, OR LIKE COVERING MATERIALS, e.g. LINOLEUM, OILCLOTH, ARTIFICIAL LEATHER, ROOFING FELT, CONSISTING OF A FIBROUS WEB COATED WITH A LAYER OF MACROMOLECULAR MATERIAL; FLEXIBLE SHEET MATERIAL NOT OTHERWISE PROVIDED FOR
- D06N3/00—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof
- D06N3/0056—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof characterised by the compounding ingredients of the macro-molecular coating
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Abstract
The invention relates to the technical field of filter bags, and discloses a filter bag for inhibiting condensation and dust adhesion and a processing technology thereof; the method comprises the following steps: placing the gelatinizer in water, heating to 80-85deg.C, and stirring for 8-12 hr; adding inorganic particles, and continuing to keep the temperature and stir for 2-4 hours to obtain a coating A; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; and (3) baking the whole body in a baking oven at 110-120 ℃ for 20-30min to obtain the filter bag for inhibiting condensation and dust adhesion.
Description
Technical Field
The invention relates to the technical field of filter bags, in particular to a filter bag for inhibiting condensation and dust adhesion and a processing technology thereof.
Background
The bag type dust collector is widely applied to industries such as coal-fired power plants, steel, cement, metal smelting, glass and the like due to the advantages of high dust collection efficiency, simple structure, convenience in maintenance and the like. However, the problem of filter bag failure caused by various factors such as oil, water vapor, temperature and the like is endlessly solved due to the fact that different actual field working conditions are complex, and the problem of "sticking a bag" is one of the most typical problems. The 'paste bag' is a phenomenon that dust adheres to the dust facing surface or the inside of a filter bag when a dust collection bag is in long-term operation and has high humidity or oily substances are in contact, so that the air permeability is reduced sharply, and the operation resistance of the dust collector is increased sharply.
The "stick-on-bag" problem is a large pain point of current failure. At present, the pasting-resistant performance of the filter bag is improved mainly by methods of Polytetrafluoroethylene (PTFE) emulsion dipping, coating, water and oil repellent agent, PTFE film coating and the like. However, the problem of sticking the bag can not be effectively improved simply by the method of dipping and coating the PTFE emulsion. The water-repellent and oil-repellent agent has too many kinds, part of the water-repellent and oil-repellent agent has poor oil-repellent effect, has poor resistance to oily smoke, is easy to lose efficacy at high temperature, causes difficulty in solving the problem of pasting bags, and can also cause damage and poor oil repellency of the film after PTFE coating film is used for a period of time and is washed by dust for a long time.
As patent CN102392355a discloses a preparation method of water-repellent oil-proof easy ash removal, the method adopts PTFE emulsion and long-chain alkyl silicone oil to carry out composite pair for common dipping treatment, and the finishing mode adopts water-repellent oil-proof of PTFE emulsion for anti-paste bag treatment. However, in practice, PTFE emulsions have a certain water-repellent and oil-repellent effect, but have a larger gap than the effect of suppressing the sticking of the paste, and thus the handling of the method of this patent results in easy sticking of the paste due to humidity or oil gas in actual field use.
Therefore, the invention provides the filter bag for inhibiting condensation and dust adhesion and the processing technology thereof.
Disclosure of Invention
The invention aims to provide a filter bag for inhibiting condensation and dust adhesion and a processing technology thereof, so as to solve the problems in the prior art.
In order to solve the technical problems, the invention provides the following technical scheme:
a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps:
s1: adding potassium hydroxide into octamethyl cyclotetrasiloxane, heating to 100-105 ℃ for reaction for 2-2.5h, adding 2,4,6, 8-tetramethyl-2, 4,6, 8-tetravinyl cyclotetrasiloxane, continuously preserving heat for reaction for 2-2.5h, and performing rotary evaporation to obtain vinyl polysiloxane; uniformly stirring vinyl modified cellulose nanocrystals, vinyl polysiloxane and sodium stearoyl lactylate, and adding deionized water for emulsification to obtain emulsion A; adding sodium dodecyl benzene sulfonate into deionized water, stirring uniformly, adding butyl acrylate, methyl methacrylate, acyloxy ethyl trimethyl ammonium chloride methacrylate and diethylene glycol divinyl ether for emulsification to obtain emulsion B; heating the emulsion B to 65-75 ℃, adding the emulsion A and ammonium persulfate, heating to 80-85 ℃ for reaction for 2-3h, and regulating the pH value to be neutral to obtain emulsion C; adding cellulose nanocrystalline into the emulsion C, and uniformly stirring to obtain a gelatinizing agent;
S2: placing the gelatinizer in water, heating to 80-85deg.C, and stirring for 8-12 hr; adding inorganic particles, and continuing to keep the temperature and stir for 2-4 hours to obtain a coating A; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; and (3) baking the whole body in a baking oven at 110-120 ℃ for 20-30min to obtain the filter bag for inhibiting condensation and dust adhesion.
Further, the preparation method of the vinyl modified cellulose nanocrystalline comprises the following steps:
adding microcrystalline cellulose into a 64wt% sulfuric acid solution, heating to 45-50 ℃ for reaction for 1.5-2h, adding ice water for stopping reaction, centrifuging, dialyzing to neutrality, and freeze-drying to obtain cellulose nanocrystalline; adding cellulose nanocrystals into N, N-dimethylformamide, uniformly stirring, heating to 105-110 ℃ under nitrogen atmosphere, adding methacrylic anhydride and pyridine, reacting for 5-6h, centrifuging, washing, and freeze-drying to obtain vinyl modified cellulose nanocrystals;
cellulose nanocrystals: the mass ratio of the methacrylic anhydride is 1 (55-60); the addition amount of the pyridine is 2-2.5wt% of the total mass of the cellulose nanocrystal and the methacrylic anhydride.
Further, octamethyl cyclotetrasiloxane: the mass ratio of the 2,4,6, 8-tetramethyl-2, 4,6, 8-tetravinyl cyclotetrasiloxane is (4-5) 1; the addition amount of the potassium hydroxide is 0.1-0.15wt% of the mass of the octamethyl cyclotetrasiloxane;
the emulsion A comprises 3-5 parts of vinyl modified cellulose nanocrystalline, 3-5 parts of vinyl polysiloxane, 2-3 parts of sodium stearoyl lactylate and 20-30 parts of deionized water according to mass fraction; the emulsion B comprises, by mass, 0.8-1 part of sodium dodecyl benzene sulfonate, 12-15 parts of butyl acrylate, 8-10 parts of methyl methacrylate, 1-2 parts of acyloxy ethyl trimethyl ammonium chloride, 0.1-0.2 part of diethylene glycol divinyl ether and 40-50 parts of deionized water; the addition amount of the cellulose nanocrystalline in the gelatinizer is 0.5-2wt% of the mass of the emulsion C;
further, the preparation method of the antifouling agent comprises the following steps:
uniformly stirring polydimethylsiloxane, toluene and Karstedt catalyst for standby; heating polyethylene glycol dimethacrylate and toluene to a reflux state for 10-15min, slowly adding the mixture into the previous polydimethylsiloxane mixture, heating to 90-95 ℃ for reacting for 2-2.5h, performing rotary evaporation, extracting, adding triethoxy hydrosilane, and performing heat preservation reaction for 1.5-2h to obtain an ethoxy end-capped multiblock polymer; uniformly stirring the ethoxy end-capped multiblock polymer, the tetraethoxysilane and the octyl triethoxysilane, adjusting the pH to 3-4, heating to 60-65 ℃, reacting for 30-45min, slowly dropwise adding deionized water, and performing hydrolytic polycondensation reaction for 5-6h to obtain the antifouling agent.
Further, the polydimethylsiloxane: polyethylene glycol dimethacrylate: the mass ratio of the triethoxy hydrosilane is 1 (1.42-1.89): 1.29-1.71); ethoxy-terminated multiblock polymers: ethyl orthosilicate: the mass ratio of the octyl triethoxysilane is 3 (1.5-2) to 1.5-2.
Further, the preparation method of the water-repellent oil-repellent agent comprises the following steps:
heating isophorone diisocyanate to 30-35 ℃ for preheating, adding hydroxyethyl methacrylate and dibutyltin dilaurate for heat preservation reaction for 6-6.5h; continuously heating to 80-85 ℃, adding 2-perfluorooctyl alcohol and dibutyltin dilaurate, and reacting for 3-3.5h under heat insulation; obtaining a fluorine-containing monomer; adding fluorine-containing monomers into butyl acetate, adding azodiisobutyronitrile under nitrogen atmosphere, heating to 65-70 ℃ for reaction for 9-10h, purifying and drying to obtain fluorine-containing polymer; adding aluminum dihydrogen phosphate into fluorine-containing polymer, and stirring uniformly to obtain water-repellent and oil-repellent agent;
further, the isophorone diisocyanate: hydroxyethyl methacrylate: the molar ratio of the 2-perfluorooctyl alcohol is 1:1:1; the addition amount of the azodiisobutyronitrile is 0.3-0.4wt% of the fluorine-containing monomer; the fluoropolymer: the mass ratio of the aluminum dihydrogen phosphate is (6-8) to (2-4).
Further, in the coating A, the inorganic particle adhesion gram weight is 5-20g/m 2 The gel forming agent has an adhesion gram weight of 1-5g/m 2 ；
Further, the inorganic particle diameter is more than or equal to 90% in the range of 50-1000 nm.
Further, the attachment thickness of the inorganic particles is 0 to 30 percent of the whole thickness of the coating of the filter bag
Further, in the coating B, the adhesion gram weight of the water-repellent and oil-repellent agent is 1-5g/m 2 The adhesion gram weight of the anti-fouling agent is 1-10g/m 2 The method comprises the steps of carrying out a first treatment on the surface of the Preferably, in the coating B, the water-repellent and oil-repellent agent has an adhesion gram weight of 2-4g/m 2 The adhesion gram weight of the anti-fouling agent is 3-7g/m 2 。
Further, the inorganic particles are any one or a combination of more of titanium dioxide, silicon dioxide and calcium carbonate; the filter bag is any one of a needled felt, a spunlaced felt and a spunbonded non-woven fabric; the preferred inorganic particle is titanium dioxide.
Compared with the prior art, the invention has the following beneficial effects:
the filter bag is treated by the water-repellent and oil-repellent agent, the anti-fouling agent, the gelatinizing agent and the inorganic particles, so that the water-repellent and oil-repellent performance can be improved, the filter bag has a better improvement effect on the paste bag performance compared with the conventional product, the dust removal ratio can reach 96%, and the filter bag cannot lose efficacy at high temperature. Meanwhile, the inorganic particles can play a role of precoating the powder cake layer, and compared with the inorganic particles before the same structure is processed, the inorganic particles can reduce the outlet concentration by 20-50%, and the cycle time is prolonged by more than 10%.
The vinyl modified cellulose nanocrystal is successfully prepared by the esterification reaction of methacrylic anhydride and cellulose nanocrystal. Vinyl modified cellulose nanocrystals, vinyl polysiloxane and methacryloyloxyethyl trimethyl ammonium chloride participate in the polymerization reaction; the vinyl modified cellulose nanocrystalline is introduced into the gelatinizer, and has the function of crosslinking points in the polymerization process by utilizing the excellent mechanical property and larger specific surface area, so that the mechanical property of the gelatinizer is greatly improved; but the molecular chain movement is limited due to the formation of a crosslinked network, showing a decrease in elongation at break; according to the invention, vinyl siloxane is introduced into the gelling agent, and the toughness of the gelling agent is enhanced by utilizing the self highly compliant organosilicon chain segment, so that the breaking elongation is improved, inorganic particles can be helped to be dispersed in the gelling agent, and the inorganic particles are uniformly adhered to the surface and shallow layer part of the filter bag, so that the effect of a precoating layer can be achieved, the filtering performance is improved, and the smoke with high initial humidity and oil can be directly resisted. The synergistic effect of the vinyl modified cellulose nanocrystalline and the vinyl siloxane further improves the heat resistance of the gelatinizer, and greatly improves the application scene of the filter bag.
According to the invention, unmodified cellulose nanocrystalline is also added into the gelatinizer, and the surface of the cellulose nanocrystalline prepared by sulfuric acid hydrolysis has higher charge density, so that on one hand, negative charges carried on the surface generate electrostatic repulsion when the cellulose nanocrystalline contacts with the anti-fouling agent and the water-repellent oil-proof agent, thereby effectively improving the aggregation phenomenon of the anti-fouling agent and the water-repellent oil-proof agent in the phase separation process, greatly improving the dispersion performance of the anti-fouling agent and the water-repellent oil-proof agent particles on the surface of the coating A, reducing the particle size, enabling the constructed micro-nano structure on the surface of the coating to be finer, effectively improving the surface roughness, and further improving the hydrophobic oleophobic property and the anti-fouling property; on the other hand, the dispersion performance of the vinyl modified cellulose nanocrystals and inorganic particles in the gelling agent is further improved by utilizing electrostatic repulsion and steric hindrance between cellulose nanocrystals.
According to the invention, the anti-fouling agent is prepared by taking polydimethylsiloxane and polyethylene glycol dimethacrylate as main raw materials through hydrosilylation, and the anti-fouling agent takes the anti-protein adsorption performance of the polyethylene glycol dimethacrylate and the low surface energy and high fouling desorption performance of the polydimethylsiloxane into consideration; the vinyl triethoxysilane is used for blocking, and is hydrolyzed and polycondensed with tetraethoxysilane, octyl triethoxysilane and deionized water, so that on one hand, the thermal stability and the hydrophobic performance of the filter bag are further improved; on the other hand, the introduction of the silicon hydroxyl groups improves the bonding force between the coating B and the coating A.
The invention takes isophorone diisocyanate as a rigid monomer, isocyanate groups at two ends of the isophorone diisocyanate respectively react with hydroxyl groups in hydroxyethyl methacrylate and 2-perfluorooctyl alcohol, then the isophorone diisocyanate is subjected to self-polymerization under the help of a catalyst, and finally the isophorone diisocyanate is blended with aluminum dihydrogen phosphate to prepare the fluorine-containing water-repellent oil-repellent agent containing the rigid unit. The addition of the aluminum dihydrogen phosphate further improves the heat resistance of the filter bag. The quaternary ammonium salt chain segment in the molecular structure of the gelatinizer is incompatible with the antifouling agent and the hydrophobic oil repellent agent chain segment, so that microphase separation of the quaternary ammonium salt chain segment and the antifouling agent and the hydrophobic oil repellent agent can be promoted, and the polydimethyl siloxane flexible chain segment in the antifouling agent can be helped to migrate in the surface direction of the coating; fluorine-containing groups in the water-repellent and oil-repellent agent also migrate like the direction of the surface of the coating during heating; rearranging the surface of the coating; on the one hand, the hydrophilic property of the polydimethylsiloxane can enhance the protein adsorption resistance and the antifouling property of the coating, the low surface free energy property of the fluorine-containing group can enhance the hydrophobic property of the coating, and the oleophobic, hydrophobic and antifouling properties of the coating are further improved by the synergistic effect of the two; on the other hand, the fluorine-containing group can migrate to the surface with the rigid unit isophorone diisocyanate in the structure in the migration process to the surface, and can cooperate with the soft chain segment polydimethylsiloxane to greatly improve the toughness of the filter bag coating.
Detailed Description
The following description of the technical solutions in the embodiments of the present invention will be clear and complete, and it is obvious that the described embodiments are only some embodiments of the present invention, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
In the following examples, microcrystalline cellulose has a particle size of 25 μm and is available from Shanghai Meilin Biochemical technologies Co., ltd; polydimethylsiloxane mn=500, purchased from Sigma-Aldrich; polyethylene glycol dimethacrylate mn=500, available from alas Ding Shiji limited; the antifouling agent is purchased from Zhejiang chemical group Co., ltd; the water-repellent oil-repellent agent is purchased from su-zhou Jiesheng new materials limited; the gellant is available from the Guangzhou Yingrui chemical technology Co., ltd; the rest of the raw materials of the inorganic particles purchased from Shanghai Liang Jiang Taibai chemical products are all commercially available.
The preparation method of the vinyl modified cellulose nanocrystalline comprises the following steps:
adding microcrystalline cellulose into a 64wt% sulfuric acid solution, heating to 45 ℃ for reaction for 1.5 hours, adding ice water for stopping the reaction, centrifuging, dialyzing to neutrality, and freeze-drying to obtain cellulose nanocrystalline; 3g of cellulose nanocrystalline is added into 150mLN, N-dimethylformamide, the mixture is stirred uniformly, the mixture is heated to 105 ℃ under nitrogen atmosphere, 180g of methacrylic anhydride and 3.66g of pyridine are added for reaction for 5 hours, and the vinyl modified cellulose nanocrystalline is obtained after centrifugation, washing and freeze drying.
Example 1: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
s2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 3:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 15%; the surface water-repellent oil-repellent agent is finally prepared with an adhesion gram weight of 1.5g/m, an anti-fouling agent adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Example 2: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
S2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 9:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared, the adhesion gram weight is 4.5g/m, the adhesion gram weight of the antifouling agent is 5g/m, the adhesion gram weight of inorganic particles is 10g/m, the adhesion thickness ratio of the inorganic particles is 25%, and the adhesion gram weight of the gelling agent is 2 g/m.
Example 3: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
s2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
Wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Example 4: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
s2: taking a water-repellent oil-proof agent and a pollution-proof agent, wherein the proportion of the water-repellent oil-proof agent to the water is 4:4:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared with the adhesion gram weight of 2g/m, the adhesion gram weight of the antifouling agent is 2g/m, the adhesion gram weight of inorganic particles is 10g/m, the adhesion thickness ratio of the inorganic particles is 25%, and the adhesion gram weight of the gelling agent is 2 g/m.
Example 5: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
s2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:18:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 9g/m, an inorganic particle adhesion gram weight is 10g/m, an inorganic particle adhesion thickness ratio is 25%, and a gelling agent adhesion gram weight is 2 g/m.
Example 6: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
S2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 2min to obtain a filter bag for inhibiting condensation and dust adhesion;
wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 35%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Example 7: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
s2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
Wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 75%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Example 8: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
s2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 8%; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Example 9: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
s2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 25%; the surface water-repellent oil-repellent agent is finally prepared with an adhesion gram weight of 1.5g/m, an anti-fouling agent adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Example 10: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
S2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of C-F bond of the water-repellent oil-repellent agent is 6, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Example 11: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:1:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
s2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
Wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Example 12: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:12:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
s2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Example 13: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
s2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles is 85% between 50 and 1000 nm; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Example 14: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 1:4:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
S2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Example 15: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 0.5:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
s2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
Wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 15%; the surface water-repellent oil-repellent agent is finally prepared with an adhesion gram weight of 2g/m, an anti-fouling agent adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 0.5 g/m.
Example 16: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 5.5:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
s2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 15%; the surface water-repellent oil-repellent agent is finally prepared with an adhesion gram weight of 2g/m, an anti-fouling agent adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 5.5 g/m.
Example 17: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
s2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
wherein the viscosity of the gelatinizer is 5000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Example 18: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: adding 0.4g of potassium hydroxide into 4g of octamethyl cyclotetrasiloxane, heating to 100 ℃ for reaction for 2 hours, adding 1g of 2,4,6, 8-tetramethyl-2, 4,6, 8-tetravinyl cyclotetrasiloxane, continuing to perform heat preservation reaction for 2 hours, and performing rotary evaporation to obtain vinyl polysiloxane; uniformly stirring 3g of vinyl modified cellulose nanocrystalline, 3g of vinyl polysiloxane and 2g of sodium stearoyl lactylate, and adding 25g of deionized water for emulsification to obtain emulsion A; adding 0.8g of sodium dodecyl benzene sulfonate into 15g of deionized water, uniformly stirring, adding 12g of butyl acrylate, 8g of methyl methacrylate, 1g of acyloxy ethyl trimethyl ammonium chloride methacrylate, 0.1g of diethylene glycol divinyl ether and 25g of deionized water, and emulsifying to obtain emulsion B; heating the emulsion B to 65 ℃, adding the emulsion A and 0.2wt% ammonium persulfate, heating to 80 ℃ for reaction for 2 hours, and regulating the pH to be neutral to obtain emulsion C; adding 1wt% of cellulose nanocrystalline into the emulsion C, uniformly stirring, and adding water for dilution to obtain a gelatinizing agent;
S2: uniformly stirring 5g of polydimethylsiloxane, 50g of toluene and 50 mu L of Karstedt catalyst for later use; 7.1g of polyethylene glycol dimethacrylate and 50g of toluene, heating to a reflux state for 10min, slowly adding the mixture into the previous polydimethylsiloxane mixture, heating to 90 ℃ for reaction for 2h, rotary steaming, extracting, adding 6.45g of triethoxy hydrosilane, and reacting for 1.5h with heat preservation to obtain an ethoxy end-capped multiblock polymer; uniformly stirring 3g of ethoxy end-capped multiblock polymer, 1.5g of tetraethoxysilane and 1.5g of octyl triethoxysilane, adjusting the pH to 3, heating to 60 ℃, reacting for 30min, slowly dropwise adding deionized water, hydrolyzing and polycondensing for 5h, and diluting with water to obtain an antifouling agent;
s3: heating 0.1mol of isophorone diisocyanate to 30 ℃ for preheating, adding 0.1mol of hydroxyethyl methacrylate and dibutyltin dilaurate for thermal insulation reaction for 6 hours; continuously heating to 80 ℃, adding 0.1mol of 2-perfluorooctyl ethanol and dibutyltin dilaurate, and reacting for 3 hours under heat preservation; obtaining a fluorine-containing monomer; adding fluorine-containing monomers into butyl acetate, adding 0.3wt% of azodiisobutyronitrile under the nitrogen atmosphere, heating to 65 ℃ for reaction for 9 hours, purifying and drying to obtain fluorine-containing polymers; adding 3g of aluminum dihydrogen phosphate into 7g of fluorine-containing polymer, uniformly stirring, and diluting with water to obtain a water-repellent oil-proof agent;
S4: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A; taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; and (3) baking the whole body in a baking oven at 110-120 ℃ for 20-30min to obtain the filter bag for inhibiting condensation and dust adhesion.
Wherein the ratio of the diameter of the inorganic particles is between 50 and 1000nm is 95 percent; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Comparative example 1: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
S2: taking a water-repellent oil-proof agent and a pollution-proof agent, wherein the proportion of the water-repellent oil-proof agent to the water is 0:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110-120 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared, the adhesion gram weight is 0g/m, the adhesion gram weight of the antifouling agent is 5g/m, the adhesion gram weight of inorganic particles is 10g/m, the adhesion thickness ratio of the inorganic particles is 25%, and the adhesion gram weight of the gelling agent is 2 g/m.
Comparative example 2: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
s2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 12:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
Wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 6g/m, an anti-fouling agent is prepared with an adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight is 10g/m, an inorganic particle adhesion thickness ratio is 25%, and a gelling agent adhesion gram weight is 2 g/m.
Comparative example 3: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
s2: taking a water-repellent oil-proof agent and a pollution-proof agent, wherein the ratio of the water-repellent oil-proof agent to the water is 4:0:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 0g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Comparative example 4: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
s2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:24:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 50%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 12g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Comparative example 5: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
S2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 10%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Comparative example 6: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A;
s2: taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110 ℃ for 20min to obtain a filter bag for inhibiting condensation and dust adhesion;
Wherein the viscosity of the gelatinizer is 2000 mPas, and the ratio of the diameter of the inorganic particles between 50 and 1000nm is 95%; the number of C in single cycle of C-F bond of the water-repellent oil-repellent agent is 8, the proportion of polysiloxane derivative in the anti-fouling agent is 90%, and the proportion of alcohol substance is 15%; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Comparative example 7: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: adding 0.4g of potassium hydroxide into 4g of octamethyl cyclotetrasiloxane, heating to 100 ℃ for reaction for 2 hours, adding 1g of 2,4,6, 8-tetramethyl-2, 4,6, 8-tetravinyl cyclotetrasiloxane, continuing to perform heat preservation reaction for 2 hours, and performing rotary evaporation to obtain vinyl polysiloxane; uniformly stirring 3g of vinyl modified cellulose nanocrystalline, 3g of vinyl polysiloxane and 2g of sodium stearoyl lactylate, and adding 25g of deionized water for emulsification to obtain emulsion A; adding 0.8g of sodium dodecyl benzene sulfonate into 15g of deionized water, uniformly stirring, adding 12g of butyl acrylate, 8g of methyl methacrylate, 1g of acyloxy ethyl trimethyl ammonium chloride methacrylate, 0.1g of diethylene glycol divinyl ether and 25g of deionized water, and emulsifying to obtain emulsion B; heating the emulsion B to 65 ℃, adding the emulsion A and 0.2wt% ammonium persulfate, heating to 80 ℃ for reaction for 2 hours, and regulating the pH to be neutral to obtain emulsion C; adding 1wt% of cellulose nanocrystalline into the emulsion C, uniformly stirring, and adding water for dilution to obtain a gelatinizing agent;
S2: uniformly stirring 5g of polydimethylsiloxane, 50g of toluene and 50 mu L of Karstedt catalyst for later use; 7.1g of polyethylene glycol dimethacrylate and 50g of toluene, heating to a reflux state for 10min, slowly adding the mixture into the previous polydimethylsiloxane mixture, heating to 90 ℃ for reaction for 2h, rotary steaming, extracting, adding 6.45g of triethoxy hydrosilane, and reacting for 1.5h with heat preservation to obtain an ethoxy end-capped multiblock polymer; uniformly stirring 3g of ethoxy end-capped multiblock polymer, 1.5g of tetraethoxysilane and 1.5g of octyl triethoxysilane, adjusting the pH to 3, heating to 60 ℃, reacting for 30min, slowly dropwise adding deionized water, hydrolyzing and polycondensing for 5h, and diluting with water to obtain an antifouling agent;
s3: heating 0.1mol of isophorone diisocyanate to 30 ℃ for preheating, adding 0.1mol of hydroxyethyl methacrylate and dibutyltin dilaurate for thermal insulation reaction for 6 hours; continuously heating to 80 ℃, adding 0.1mol of 2-perfluorooctyl ethanol and dibutyltin dilaurate, and reacting for 3 hours under heat preservation; obtaining a fluorine-containing monomer; adding fluorine-containing monomers into butyl acetate, adding 0.3wt% of azodiisobutyronitrile under the nitrogen atmosphere, heating to 65 ℃ for reaction for 9 hours, purifying and drying to obtain fluorine-containing polymers; adding 3g of aluminum dihydrogen phosphate into 7g of fluorine-containing polymer, uniformly stirring, and diluting with water to obtain a water-repellent oil-proof agent;
S4: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A; taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; and (3) baking the whole body in a baking oven at 110-120 ℃ for 20-30min to obtain the filter bag for inhibiting condensation and dust adhesion.
Wherein the ratio of the diameter of the inorganic particles is between 50 and 1000nm is 95 percent; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
Comparative example 8: a processing technology of a filter bag for inhibiting condensation and dust adhesion comprises the following steps: s1: adding 0.4g of potassium hydroxide into 4g of octamethyl cyclotetrasiloxane, heating to 100 ℃ for reaction for 2 hours, adding 1g of 2,4,6, 8-tetramethyl-2, 4,6, 8-tetravinyl cyclotetrasiloxane, continuing to perform heat preservation reaction for 2 hours, and performing rotary evaporation to obtain vinyl polysiloxane; uniformly stirring 3g of vinyl modified cellulose nanocrystalline, 3g of vinyl polysiloxane and 2g of sodium stearoyl lactylate, and adding 25g of deionized water for emulsification to obtain emulsion A; adding 0.8g of sodium dodecyl benzene sulfonate into 15g of deionized water, uniformly stirring, adding 12g of butyl acrylate, 8g of methyl methacrylate, 1g of acyloxy ethyl trimethyl ammonium chloride methacrylate, 0.1g of diethylene glycol divinyl ether and 25g of deionized water, and emulsifying to obtain emulsion B; heating the emulsion B to 65 ℃, adding the emulsion A and 0.2wt% of ammonium persulfate, heating to 80 ℃ for reaction for 2 hours, adjusting the pH to be neutral, and adding water for dilution to obtain a gelatinizing agent;
S2: uniformly stirring 5g of polydimethylsiloxane, 50g of toluene and 50 mu L of Karstedt catalyst for later use; 7.1g of polyethylene glycol dimethacrylate and 50g of toluene, heating to a reflux state for 10min, slowly adding the mixture into the previous polydimethylsiloxane mixture, heating to 90 ℃ for reaction for 2h, rotary steaming, extracting, adding 6.45g of triethoxy hydrosilane, and reacting for 1.5h with heat preservation to obtain an ethoxy end-capped multiblock polymer; uniformly stirring 3g of ethoxy end-capped multiblock polymer, 1.5g of tetraethoxysilane and 1.5g of octyl triethoxysilane, adjusting the pH to 3, heating to 60 ℃, reacting for 30min, slowly dropwise adding deionized water, hydrolyzing and polycondensing for 5h, and diluting with water to obtain an antifouling agent;
s3: heating 0.1mol of isophorone diisocyanate to 30 ℃ for preheating, adding 0.1mol of hydroxyethyl methacrylate and dibutyltin dilaurate for thermal insulation reaction for 6 hours; continuously heating to 80 ℃, adding 0.1mol of 2-perfluorooctyl ethanol and dibutyltin dilaurate, and reacting for 3 hours under heat preservation; obtaining a fluorine-containing monomer; adding fluorine-containing monomers into butyl acetate, adding 0.3wt% of azodiisobutyronitrile under the nitrogen atmosphere, heating to 65 ℃ for reaction for 9 hours, purifying and drying to obtain fluorine-containing polymers; adding 3g of aluminum dihydrogen phosphate into 7g of fluorine-containing polymer, uniformly stirring, and diluting with water to obtain a water-repellent oil-proof agent;
S4: taking a gelatinizing agent, inorganic particles and water according to the proportion of 2:5:50 respectively; the gelatinizer is put into water, heated to 80 ℃ and stirred for 12 hours; adding inorganic particles, and continuing to keep the temperature and stir for 2 hours to obtain a coating A; taking a water-repellent oil-repellent agent and a pollution-preventive agent, wherein the proportion of the water-repellent oil-repellent agent to the water is 4:10:40 respectively; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; and (3) baking the whole body in a baking oven at 110-120 ℃ for 20-30min to obtain the filter bag for inhibiting condensation and dust adhesion.
Wherein the ratio of the diameter of the inorganic particles is between 50 and 1000nm is 95 percent; the number of C in single cycle of the water-repellent and oil-repellent agent C-F bond is 8; finally, the surface water-repellent oil-repellent agent is prepared with an adhesion gram weight of 2g/m, an anti-fouling agent is prepared with an adhesion gram weight of 5g/m, an inorganic particle adhesion gram weight of 10g/m, an inorganic particle adhesion thickness ratio of 25%, and a gelling agent adhesion gram weight of 2 g/m.
And (3) testing: water repellency properties: according to GB/T4745-2012, at least 18 x 18cm is leveled, and is clamped on a clamp (the clamp and the horizontal plane form an angle of 45 degrees) after humidity adjustment, the front face is upward, 250ml of water is rapidly and stably poured into a funnel, and the funnel is continuously sprayed for 25-30 s. After stopping spraying, the clamp holder with the sample is taken off, and the sample is tapped once horizontally against the solid hard object from the front surface downwards, and then the sample is tapped once again by rotating 180 degrees. And finally, evaluating according to the water dipping evaluation grade.
For this case: and the water repellent effect is more than or equal to grade 4 and is qualified.
Specific test performance data are shown in tables 1-3 below.
Oil repellency: according to GB/T19977-2014, 3 samples with the size of 20cm are taken, the samples are flatly paved on a liquid suction pad with a smooth horizontal surface from the front surface upwards, 5 small drops (with the volume of about 0.05 ml) are dripped on a tested sample from the oil liquid with the number of 1, the interval between the liquid drops is 4cm, the distance between the mouth of a dropper and the surface of the sample is 6mm, the liquid drops are observed for 30 s+/-2 s at an angle of 45 degrees, and the evaluation is carried out according to an evaluation standard and a comparison chart.
For this case: the oil-repellent effect is more than or equal to 6 grades and is qualified.
Specific test performance data are shown in tables 1-3 below.
Dust removal ratio: the dust removal ratio refers to the ratio of the absolute value of the difference between the initial adhesion amount and the final adhesion amount of dust on the surface of the filter bag to the initial adhesion amount. According to GB/T30159.1-2013, a square 235cm + -5 cm overturning box (containing a rotating shaft), a test cylinder and a sample fixing plate are prepared, the inner diameter of the cylinder body is 90 + -0.5 mm, the height is 50 + -0.5 mm, the thickness is 3 + -0.5 mm, the cylinder wall is uniformly provided with 3 rectangular holes, the arc length in each hole is 50 + -0.5 mm, and the height is 80 + -0.5 mm, and the cylinder cover is tightly attached to the cylinder body. The length of the sample fixing piece is the same as the outer diameter circumference of the cylinder body, the width is 93+/-0.5 mm, and 3 cuboid convex parts with the thickness of 3+/-0.5 mm are arranged on the sample fixing piece. Preparing 30cm of samples, placing the samples on a sample fixing sheet with the front face facing upwards to cover 3 convex parts, coating the cylinder body, adding 50g of dust into the cylinder bottom, covering the cylinder cover, fixing the cylinder cover on a rotating shaft, and placing the cylinder cover into a turnover box. The overturning is stopped 200 times. Taking out the test weight, calculating the initial adhesion amount, then spraying the back of the sample for 10 times at intervals of 5s by using a pulse air gun, testing the weight again, calculating the final adhesion amount, and finally calculating the dust removal ratio.
The dust removal ratio is more than or equal to 96% and is qualified.
Specific test performance data are shown in tables 1-3 below.
Gram weight increase: the grammage increment refers to the difference between the weight of the treated sample and the initial sample weight. The weight of a 25cm by 20cm sample was measured with a balance (precision 0.01 g), and the mass per unit area expressed in g/m square was obtained by multiplying 20. The weight of the treated sample was retested and the difference was the increase in grammage.
Specific test performance data are shown in tables 1-3 below.
Particle penetration depth ratio: and (3) observing and testing the section of the filter bag by adopting a Scanning Electron Microscope (SEM), wherein the magnification is 50-600 times, sequentially and uniformly finding out 5 points from left to right for testing, marking out the size value of the thickness of the fiber surface with particles attached, calculating an average value, and then calculating the ratio of the average value to the whole thickness.
Specific test performance data are shown in tables 1-3 below.
VDI3926 capture efficiency, outlet concentration, pressure loss, cycle time: the performance of the filter material was determined based on the standard of VDI3926, the size of the test sample being 150mm in diameter. Concentration of fed dustAt 5.0+ -0.5 g/m 3 The filtration wind speed was 2 m/mm (air volume 1.85m 3/h). The experimental sequence was initial 30 rounds + stabilization 5000 rounds + final 30 rounds. The initial 30 rounds and the final 30 rounds are as follows: as the running time is prolonged, the pressure difference across the filter material gradually increases, when the pressure difference reaches 1000Pa, the pulse air cleans the dust on the surface of the filter material, then the next process is carried out, the process is repeated for 30 times, the change of the experiment time (t/s) and the pressure is recorded in the experiment process, and meanwhile, the weight M (g) of the dust penetrating through the filter material is weighed. The stabilization process is to remove ash from the filter material at intervals of 5s, the ash removal pressure is 5bar, and the ash removal times are 5000 times. The calculation formula of the outlet dust concentration and the trapping efficiency is as follows:
Outlet dust concentration c=weight of dust passing through the filter material M/(1.85 x time t/3600), the unit of outlet dust concentration C being g/M 3 ；
Trapping efficiency= (1-outlet dust concentration C/5) ×100%;
the pressure loss is automatically recorded by the equipment after the last injection of the last 30 times;
the cycle time is the total time spent for the last 30 rounds.
For this case: and the outlet concentration of VDI is less than or equal to 0.025mg/Nm3, and the cycle time of VDI is more than or equal to 5500 s.
Specific test performance data are shown in tables 1-3 below.
TABLE 1
TABLE 2
TABLE 3 Table 3
Conclusion: (1) The data of examples 1-7 and example 18 fully illustrate that all performance indexes are better in a specified range;
(2) As is clear from examples 3, 8 and 9, the alcohol content of example 3 was in the preferred range under the same conditions, and the resulting antifouling effect was better and the dust removal ratio was higher.
(3) As is clear from examples 3 and 10, the number of the water/oil repellent agents C in example 3 is a preferable value, and therefore the water/oil repellency is higher.
(4) From examples 3, 11 and 12, the inorganic particles of example 3 have an adhesion grammage within a preferred range, and the resulting water-repellent oil-repellent grade is higher, the VDI outlet concentration is lower, and the cycle time is longer.
(5) From examples 3 and 13, example 13 showed that the inorganic particle ratio was less than 90% and the VDI cycle time was relatively short.
(6) From examples 3 and 14, the inorganic particles of example 14 have a large adhesion thickness and a short VDI cycle time.
(7) From examples 3, 15, and 16, it is clear that the greater or lesser grammage of the gellant of examples 15 and 16 tends to result in an increase in VDI outlet concentration and a relatively shorter cycle time.
(8) From examples 3 and 17, it is apparent that the viscosity of the gelling agent of example 17 is too high, which results in an increase in the outlet concentration and a reduction in the cycle time.
(9) From example 3, comparative examples 1 and 2 show that the water and oil repellent agent has a low gram weight and a poor water and oil repellent effect, and that the water and oil repellent agent has a too high gram weight and poor dust removal ability, and the VDI performance index is poor.
(10) From example 3, comparative examples 3 and 4 show that the stain-proofing agent has too low gram weight and very low dust removal ability, and the stain-proofing agent has too high gram weight, and the water-repellent and oil-repellent ability is affected, and the water-repellent and oil-repellent ability is deteriorated, and the VDI performance index is poor.
(11) From example 3, comparative examples 5 and 6 show that the ratio of polysiloxane derivative is too low, the dust removal ratio is low, and the ratio of polysiloxane derivative is too high, and the VDI filtration performance is deteriorated.
(12) From examples 3 and 18, comparative examples 7 and 8, it is clear that the quaternary ammonium salt segment was not incorporated in comparative example 7; the absence of the addition of the unmodified cellulose nanocrystals in comparative example 8 resulted in a decrease in the water and oil repellency properties.
Finally, it should be noted that: the foregoing description is only a preferred embodiment of the present invention, and the present invention is not limited thereto, but it is to be understood that modifications and equivalents of some of the technical features described in the foregoing embodiments may be made by those skilled in the art, although the present invention has been described in detail with reference to the foregoing embodiments. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (9)
1. A processing technology of a filter bag for inhibiting condensation and dust adhesion is characterized in that: comprises the following steps:
placing the gelatinizer in water, heating to 80-85deg.C, and stirring for 8-12 hr; adding inorganic particles, and continuing to keep the temperature and stir for 2-4 hours to obtain a coating A; uniformly stirring an antifouling agent, a water-repellent oil-repellent agent and a water chamber at the temperature to obtain a coating B; coating the coating A on the surface of the filter bag to obtain a coating A; spraying the coating B on the surface of the coating A to obtain a coating B; baking the whole body in a baking oven at 110-120 ℃ for 20-30min to obtain a filter bag for inhibiting condensation and dust adhesion;
The preparation method of the gelling agent comprises the following steps:
adding microcrystalline cellulose into sulfuric acid solution, heating to 45-50deg.C for reacting for 1.5-2h, adding ice water to terminate the reaction, centrifuging, dialyzing to neutrality, and lyophilizing to obtain cellulose nanocrystalline; adding cellulose nanocrystals into N, N-dimethylformamide, uniformly stirring, heating to 105-110 ℃ under nitrogen atmosphere, adding methacrylic anhydride and pyridine, reacting for 5-6h, centrifuging, washing, and freeze-drying to obtain vinyl modified cellulose nanocrystals;
adding potassium hydroxide into octamethyl cyclotetrasiloxane, heating to 100-105 ℃ for reaction for 2-2.5h, adding 2,4,6, 8-tetramethyl-2, 4,6, 8-tetravinyl cyclotetrasiloxane, continuously preserving heat for reaction for 2-2.5h, and performing rotary evaporation to obtain vinyl polysiloxane; uniformly stirring vinyl polysiloxane, vinyl modified cellulose nanocrystalline and sodium stearoyl lactylate, adding deionized water for emulsification to obtain emulsion A; adding sodium dodecyl benzene sulfonate into deionized water, stirring uniformly, adding butyl acrylate, methyl methacrylate, acyloxy ethyl trimethyl ammonium chloride methacrylate and diethylene glycol divinyl ether for emulsification to obtain emulsion B; heating the emulsion B to 65-75 ℃, adding the emulsion A and ammonium persulfate, heating to 80-85 ℃ for reaction for 2-3h, and regulating the pH value to be neutral to obtain emulsion C; adding cellulose nanocrystalline into the emulsion C, and uniformly stirring to obtain a gelatinizing agent;
Cellulose nanocrystals: the mass ratio of the methacrylic anhydride is 1 (55-60); the addition amount of the pyridine is 2-2.5wt% of the total mass of the cellulose nanocrystal and the methacrylic anhydride.
2. The process for manufacturing the filter bag capable of inhibiting condensation and dust adhesion according to claim 1, wherein:
octamethyl cyclotetrasiloxane: the mass ratio of the 2,4,6, 8-tetramethyl-2, 4,6, 8-tetravinyl cyclotetrasiloxane is (4-5) 1; the addition amount of the potassium hydroxide is 0.1-0.15wt% of the mass of the octamethyl cyclotetrasiloxane;
the emulsion A comprises 3-5 parts of vinyl modified cellulose nanocrystalline, 3-5 parts of vinyl polysiloxane, 2-3 parts of sodium stearoyl lactylate and 20-30 parts of deionized water according to mass fraction; the emulsion B comprises, by mass, 0.8-1 part of sodium dodecyl benzene sulfonate, 12-15 parts of butyl acrylate, 8-10 parts of methyl methacrylate, 1-2 parts of acyloxy ethyl trimethyl ammonium chloride, 0.1-0.2 part of diethylene glycol divinyl ether and 40-50 parts of deionized water; the addition amount of the cellulose nanocrystalline in the gelatinizer is 0.5-2wt% of the mass of the emulsion C.
3. The process for manufacturing the filter bag capable of inhibiting condensation and dust adhesion according to claim 1, wherein: the preparation method of the antifouling agent comprises the following steps:
Uniformly stirring polydimethylsiloxane, toluene and Karstedt catalyst for standby; heating polyethylene glycol dimethacrylate and toluene to a reflux state for 10-15min, slowly adding the mixture into the previous polydimethylsiloxane mixture, heating to 90-95 ℃ for reacting for 2-2.5h, performing rotary evaporation, extracting, adding triethoxy hydrosilane, and performing heat preservation reaction for 1.5-2h to obtain an ethoxy end-capped multiblock polymer; uniformly stirring the ethoxy end-capped multiblock polymer, the tetraethoxysilane and the octyl triethoxysilane, adjusting the pH to 3-4, heating to 60-65 ℃, reacting for 30-45min, slowly dropwise adding deionized water, and performing hydrolytic polycondensation reaction for 5-6h to obtain the antifouling agent.
4. A process for manufacturing a filter bag for suppressing dew condensation and dust adhesion according to claim 3, wherein: polydimethyl siloxane: polyethylene glycol dimethacrylate: the mass ratio of the triethoxy hydrosilane is 1 (1.42-1.89): 1.29-1.71); ethoxy-terminated multiblock polymers: ethyl orthosilicate: the mass ratio of the octyl triethoxysilane is 3 (1.5-2) to 1.5-2.
5. The process for manufacturing the filter bag capable of inhibiting condensation and dust adhesion according to claim 1, wherein: the preparation method of the water-repellent oil-repellent agent comprises the following steps:
Heating isophorone diisocyanate to 30-35 ℃ for preheating, adding hydroxyethyl methacrylate and dibutyltin dilaurate for heat preservation reaction for 6-6.5h; continuously heating to 80-85 ℃, adding 2-perfluorooctyl alcohol and dibutyltin dilaurate, and reacting for 3-3.5h under heat insulation; obtaining a fluorine-containing monomer; adding fluorine-containing monomers into butyl acetate, adding azodiisobutyronitrile under nitrogen atmosphere, heating to 65-70 ℃ for reaction for 9-10h, purifying and drying to obtain fluorine-containing polymer; adding aluminum dihydrogen phosphate into the fluorine-containing polymer, and stirring uniformly to obtain the water-repellent oil-repellent agent.
6. The process for manufacturing the filter bag capable of inhibiting condensation and dust adhesion according to claim 5, wherein:
isophorone diisocyanate: hydroxyethyl methacrylate: the molar ratio of the 2-perfluorooctyl alcohol is 1:1:1; the addition amount of the azodiisobutyronitrile is 0.3-0.4wt% of the fluorine-containing monomer; the fluoropolymer: the mass ratio of the aluminum dihydrogen phosphate is (6-8) to (2-4).
7. The process for manufacturing the filter bag capable of inhibiting condensation and dust adhesion according to claim 1, wherein: in the coating A, the inorganic particle adhesion gram weight is 5-20g/m 2 The gel forming agent has an adhesion gram weight of 1-5g/m 2 The method comprises the steps of carrying out a first treatment on the surface of the In the coating B, the adhesion gram weight of the water-repellent oil-repellent agent is 1-5g/m 2 The adhesion gram weight of the anti-fouling agent is 1-10g/m 2 The method comprises the steps of carrying out a first treatment on the surface of the The ratio of the diameter of the inorganic particles is 50-1000 nm and is more than or equal to 90%; the attachment thickness of the inorganic particles is 0-30% of the whole thickness of the filter bag coating.
8. The process for manufacturing the filter bag capable of inhibiting condensation and dust adhesion according to claim 1, wherein: the inorganic particles are any one or a combination of more of titanium dioxide, silicon dioxide and calcium carbonate; the filter bag is any one of a needled felt, a spunlaced felt and a spunbonded non-woven fabric.
9. The filter bag for inhibiting condensation and dust adhesion according to any one of claims 1 to 8, which is produced by a process for producing the filter bag for inhibiting condensation and dust adhesion.
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| CN102417575A (en) * | 2011-11-01 | 2012-04-18 | 吴江市北厍盛源纺织品助剂厂 | Preparation method of fluorine-containing aqueous polyurethane water-repellent oil-repellent finishing agent |
| CN102504121A (en) * | 2011-11-01 | 2012-06-20 | 吴江市北厍盛源纺织品助剂厂 | Preparation method of fluorine-containing water-based polyurethane film-formation crosslinking agent |
| CN103483546A (en) * | 2013-09-26 | 2014-01-01 | 南京年吉冷冻食品有限公司 | Preparation method for water-repellent oil-repellent fluorinated polyurethane rigid foamed plastic |
| CN108797201A (en) * | 2018-06-11 | 2018-11-13 | 华东理工大学 | A kind of corrugation paper gluing agents and preparation method thereof |
| CN109054805A (en) * | 2018-07-12 | 2018-12-21 | 青岛科技大学 | A kind of preparation method of the fluorescence cholesteric phase Cellulose nanocrystal body thin film with Acid-base Gas response |
| CN110938211A (en) * | 2019-10-18 | 2020-03-31 | 陕西科技大学 | Method for modifying cellulose nanocrystal by using photo-response fluorine-containing amphiphilic block copolymer |
| CN112552869A (en) * | 2020-12-15 | 2021-03-26 | 佛山巨马新材料有限公司 | Preparation method of bonding adhesive for heat-insulation and decoration integrated plate |
| CN116253972A (en) * | 2023-02-24 | 2023-06-13 | 苏州辰鹏电子新材料有限公司 | Preparation method of reinforced PBT composite material |
| CN116716761A (en) * | 2023-06-29 | 2023-09-08 | 江苏宸煦新材料科技有限公司 | Light and thin release paper for outdoor exhibition and preparation process thereof |
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